FIELD OF THE INVENTION
[0001] This invention relates to molding operations. In one aspect, the invention relates
to the formation of articles through the use of injection molding techniques while
in another aspect, the invention relates to the formation of such articles in a manner
that allows for off-mold curing. In yet another aspect, the invention relates to a
method of feeding a two-component reactive system to an extruder designed for limited
mixing while in still another aspect, the invention relates to a method of forming
a mix of a base compound and a catalyst prior to feeding the mix to an extruder.
BACKGROUND OF THE INVENTION
[0002] Siloxane-modified polyolefin elastomers are under development for use in the manufacture
of power cable accessories, e.g., cable joints, splices, separable connectors, cable
termination, etc., by injection molding. These new polymers offer the possibility
of injecting thick parts in a thermoplastic mode, de-molding the part, and storing
it for latent cure off-mold under ambient conditions, i.e., without the need for external
moisture or heat. This approach has the potential of substantially cutting the manufacturing
cycle time for making these parts.
[0003] This new technology is a two-component system comprising (1) a polyolefin containing
silane functionality in combination with a hydroxy-terminated silicone polymer, or
a blend of a vinyl silane, polyolefin, peroxide and a hydroxy-terminated silicone
polymer, and (2) a catalyst masterbatch, i.e., a catalyst carried in a suitable base
polymer. These components need to be adequately blended with one another in a melt
mixing operation prior to the injection step to ensure efficient and uniform crosslinking.
[0004] One potential challenge for the implementation of this technology is that the current
injection molding manufacturing process relies on rubber injection molding equipment
in which the material is first roll-milled and then shaped into a strip, i.e., tape,
for feeding into an extruder mounted on the molding machine. These machines are typically
fitted with rubber extruders which are designed for simple masticating and pressurization.
These extruders are typically short in length, and thus have limited, if any, mixing
capability.
[0005] Accordingly, a need exists for a method by which the reactive base compound and catalyst
masterbatch are delivered to the injection molding machine without equipment modification
and with minimum interaction between the two components prior to feeding to the molding
machine so as to avoid premature reaction (scorch) of the components in the melt.
SUMMARY OF THE INVENTION
[0006] In one embodiment the invention is a tape comprising (A) a first ribbon comprising
a first compound, and (B) a second ribbon comprising a second compound, the second
ribbon carried on the first ribbon and the first and second compounds reactive with
one another under ambient conditions of 23°C and atmospheric pressure, wherein the
first compound is a crosslinkable resin, and the second compound is a catalyst that
promotes the cure of the crosslinkable resin under ambient conditions of 23°C and
atmospheric pressure. The first compound is a crosslinkable resin, e.g., a polyolefin
comprising cure sites.
[0007] In one preferred embodiment the invention is a tape comprising (A) a first ribbon
comprising (1)(a) a polyolefin containing at least one silane functionality, and (1)(b)
a hydroxy-terminated silicone polymer, or (2) a blend of a vinyl silane, polyolefin,
organic initiator, e.g., a peroxide, and a hydroxy-terminated silicone polymer, and
(B) a second ribbon comprising a catalyst masterbatch, the second ribbon carried on
the first ribbon. In one preferred embodiment the first and second ribbons are in
direct contact with one another while in another preferred embodiment, the first and
second ribbons are separated by a third component, typically a third ribbon intermediate
between the first and second ribbons. In one preferred embodiment, the third component
is an adhesive. In one preferred embodiment the third component is a barrier resin.
In one preferred embodiment the third component is both an adhesive and a barrier
resin.
[0008] In one preferred embodiment, the first ribbon comprises a groove shaped and sized
to receive and hold the second ribbon. Preferably the groove is in the machine direction
of the tape, and the groove can be continuous or intermittent. In other embodiments
the peroxide may reside in the second and/or third ribbon in addition to or in substitution
for residing in the first ribbon.
[0009] A process for making a tape comprising (A) a first ribbon comprising (1)(a) a polyolefin
containing at least one silane functionality, and (1)(b) a hydroxy-terminated silicone
polymer, or (2) a blend of a vinyl silane, polyolefin, organic initiator and a hydroxy-terminated
silicone polymer, and (B) a second ribbon comprising a catalyst masterbatch, the second
ribbon carried on the first ribbon, comprises the steps of (i) forming, e.g., extruding,
the first ribbon, (ii) forming, e.g., extruding, the second ribbon, and (iii) joining,
e.g., physical compression, chemical adhesion, etc., the first and second ribbons.
In one embodiment the first and second ribbons are co-extruded. In one embodiment
the first ribbon is extruded with a machine-direction groove and allowed to solidify,
and then the second ribbon is formed (e.g., extruded), solidified, and then fitted
into the groove of the first ribbon, with or without the aid of an adhesive. In one
embodiment a third component is placed between the first and second ribbons. In one
embodiment all three components are co-extruded and joined to one another in a single
operation.
[0010] A tape comprising (A) a ribbon comprising (1)(a) a polyolefin containing at least
one silane functionality, and (1)(b) a hydroxy-terminated silicone polymer, or (2)
a blend of a vinyl silane, polyolefin, organic initiator and a hydroxy-terminated
silicone polymer, and (B) a second component comprising a catalyst masterbatch dosed,
i.e., sprayed, onto the ribbon is also provided. In one embodiment the catalyst masterbatch
is dosed onto the ribbon just prior to feeding the ribbon into an extruder.
[0011] A multilayered tape comprising (A) a first layer comprising (1)(a) a polyolefin containing
at least one silane functionality, and (1)(b) a hydroxy-terminated silicone polymer,
or (2) a blend of a vinyl silane, polyolefin, organic initiator and a hydroxy-terminated
silicone polymer, and (B) a second layer comprising a catalyst masterbatch, the second
layer carried on the first ribbon, and (C) optionally an intermediate layer between
the first and second layers is provided. In one embodiment the intermediate layer
comprises a material that is not porous to the materials of the first and second layers
and thus serves as a barrier layer between the first and second layers.
[0012] A process for making injection molded articles, comprises feeding into an injection
molding machine a tape comprising (A) a first ribbon comprising (1)(a) a polyolefin
containing at least one silane functionality, and (1)(b) a hydroxy-terminated silicone
polymer, or (2) a blend of a vinyl silane, polyolefin, organic initiator and a hydroxy-terminated
silicone polymer, and (B) a second component comprising a catalyst masterbatch, the
second component carried on the first ribbon. In one embodiment, the first ribbon
comprises a machine-direction groove, and the second component is in the form of a
ribbon that is fitted into the groove of the first ribbon. In one embodiment, the
second component is sprayed onto the first ribbon at the time the first ribbon is
fed into the injection molding machine. In one embodiment the second component is
dosed directly into the injection molding machine simultaneously with the feeding
of the first ribbon to the injection molding machine, as opposed to dosing, e.g.,
spraying, the first ribbon with the second component.
[0013] The tapes of the invention provide an advantage over a single tape made by melt blending
(A) a polyolefin containing silane functionality in combination with a hydroxy-terminated
silicone polymer, or a blend of a vinyl silane, polyolefin, peroxide organic initiator
and a hydroxy-terminated silicone polymer, with (B) a catalyst masterbatch, because
the single tape made by melt blending the two components will have a short shelf-life
and likely require the tape to be made at the injection molding site immediately prior
to use because of limited storage life. The tapes of the invention will also provide
an advantage over individual tapes of the first and second components and then individually
feeding these tapes to an injection extruder because simultaneous, consistent feeding
of these tapes at the proper ratio is problematic at best which, in turn, can lead
to loss of catalyst feed.
[0014] The tapes of this invention allow the delivery of a consistent mixture of resin and
catalyst to an injection molding extruder. These tapes can be made off-line and supplied
to a remote molding operation, and these tapes and methods eliminate the need for
equipment modification.
BRIEF DESCRIPTION OF THE DRAWINGS
[0015]
Figure 1A is a top plan view of a base resin tape or ribbon.
Figure 1B is a top plan view of a base resin ribbon comprising a continuous, machine-direction
groove.
Figure 1C is a top plan view of a base resin ribbon comprising a discontinuous or
intermittent, machine-direction groove.
Figure ID is a top plan view of a base resin ribbon comprising a series of cross-direction
grooves.
Figure 2A is a top plan view of the ribbon of Figure 1B with a catalyst masterbatch
continuous ribbon fitted into the machine-direction groove.
Figure 2B is a top plan view of the ribbon of Figure 1B with a catalyst masterbatch
discontinuous ribbon fitted into the machine-direction groove.
Figure 3 is a cross-sectional view of a three layer tape comprising a catalyst masterbatch
layer and a base resin layer separated by a barrier layer.
Figure 4 is a schematic of a sequence of process steps comprising dosing a base resin
ribbon with a catalyst as the base resin ribbon layer is fed to an injection molding
extruder.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT
Definitions
[0016] All references to the Periodic Table of the Elements refer to the Periodic Table
of the Elements published and copyrighted by CRC Press, Inc., 2003. Also, any references
to a Group or Groups shall be to the Group or Groups reflected in this Periodic Table
of the Elements using the IUPAC system for numbering groups. Unless stated to the
contrary, implicit from the context, or customary in the art, all parts and percents
are based on weight and all test methods are current as of the filing date of this
disclosure. For purposes of United States patent practice, the contents of any referenced
patent, patent application or publication are incorporated by reference in their entirety
(or its equivalent US version is so incorporated by reference) especially with respect
to the disclosure of synthetic techniques, product and processing designs, polymers,
catalysts, definitions (to the extent not inconsistent with any definitions specifically
provided in this disclosure), and general knowledge in the art.
[0017] The numerical ranges in this disclosure are approximate, and thus may include values
outside of the range unless otherwise indicated. Numerical ranges include all values
from and including the lower and the upper values, in increments of one unit, provided
that there is a separation of at least two units between any lower value and any higher
value. As an example, if a compositional, physical or other property, such as, for
example, molecular weight, viscosity, melt index, etc., is from 100 to 1,000, it is
intended that all individual values, such as 100, 101, 102, etc., and sub ranges,
such as 100 to 144, 155 to 170, 197 to 200, etc., are expressly enumerated. For ranges
containing values which are less than one or containing fractional numbers greater
than one (e.g., 1.1, 1.5, etc.), one unit is considered to be 0.0001, 0.001, 0.01
or 0.1, as appropriate. For ranges containing single digit numbers less than ten (e.g.,
1 to 5), one unit is typically considered to be 0.1. These are only examples of what
is specifically intended, and all possible combinations of numerical values between
the lowest value and the highest value enumerated, are to be considered to be expressly
stated in this disclosure. Numerical ranges are provided within this disclosure for,
among other things, the amount of catalyst in the masterbatch, the relative amounts
of base resin and catalyst masterbatch in the tape, and various temperatures and other
process ranges.
[0018] As used with respect to a chemical compound, unless specifically indicated otherwise,
the singular includes all isomeric forms and vice versa (for example, "hexane", includes
all isomers of hexane individually or collectively). The terms "compound" and "complex"
are used interchangeably to refer to organic-, inorganic- and organometal compounds.
The term, "atom" refers to the smallest constituent of an element regardless of ionic
state, that is, whether or not the same bears a charge or partial charge or is bonded
to another atom. The term "amorphous" refers to a polymer lacking a crystalline melting
point as determined by differential scanning calorimetry (DSC) or equivalent technique.
[0019] "Composition" and like terms mean a mixture or blend of two or more components. For
example, in the context of preparing a silane-grafted ethylene polymer, a composition
would include at least one ethylene polymer, at least one vinyl silane, and at least
one free radical initiator. In the context of preparing a cable sheath or other article
of manufacture, a composition would include an ethylene-vinylsilane copolymer, a catalyst
cure system and any desired additives such as lubricant, fillers, anti-oxidants and
the like.
[0020] "Blend," "polymer blend" and like terms mean a blend of two or more polymers. Such
a blend may or may not be miscible. Such a blend may or may not be phase separated.
Such a blend may or may not contain one or more domain configurations, as determined
from transmission electron spectroscopy, light scattering, x-ray scattering, and any
other method known in the art.
[0021] "Polymer" means a polymeric compound prepared by polymerizing monomers, whether of
the same or a different type. The generic term polymer thus embraces the term homopolymer,
usually employed to refer to polymers prepared from only one type of monomer, and
the term interpolymer as defined below. It also embraces all forms of interpolymers,
e.g., random, block, homogeneous, heterogeneous, etc. The terms "ethylene/a-olefin
polymer" and "propylene/a-olefin polymer" are indicative of interpolymers as described
below.
[0022] "Interpolymer" and "copolymer" mean a polymer prepared by the polymerization of at
least two different types of monomers. These generic terms include both classical
copolymers, i.e., polymers prepared from two different types of monomers, and polymers
prepared from more than two different types of monomers, e.g., terpolymers, tetrapolymers,
etc.
[0023] "Polyolefin", "olefinic polymer", "olefinic interpolymer", and like terms mean a
polymer derived from simple olefins. Representative polyolefins include polyethylene,
polypropylene, polybutene, polyisoprene and their various interpolymers.
[0024] "Base resin", "base compound" and like terms mean a composition comprising a polyolefin
containing silane functionality in combination with a hydroxy-terminated silicone
polymer, or a blend of a vinyl silane, polyolefin, optionally an organic initiator
and a hydroxy-terminated silicone polymer.
[0025] "Catalyst masterbatch" and like terms mean a composition comprising (i) a catalyst
to promote a reaction of the polyolefin containing silane functionality with the hydroxy-terminated
silicone polymer, and (ii) a carrier resin. Typically the carrier resin is the same
as the polyolefin, without the silane functionality, in the base resin. Alternatively,
the carrier resin can be a resin different from the base resin or a solvent, i.e.,
a material that improves the ability the catalyst to mix with the base polymer in
the injection molding step.
[0026] "Ribbon", "tape" and like terms mean a narrow band or strip of material, usually
polymeric material, of indefinite length. Tape and ribbon are often used interchangeably.
A ribbon can comprise a single layer, or multiple micro-layers such as those described
in USP
5,094,793. A tape can comprise a single ribbon or two or more ribbons.
[0027] Although the invention is described primarily in terms of a polyolefin containing
at least one silane functionality and a catalyst masterbatch, the invention applies
to any two materials or compounds that are reactive with one another under ambient
conditions. As such, other polymers can be substituted for the polyolefin and other
compounds can be substituted for the catalyst masterbatch.
Polyolefin
[0028] The density of the polyolefins used in the practice of this invention, either in
the base resin or in the masterbatch, can range before modification with silane or
other functionality from 0.855 or less to 0.960 or more grams per cubic centimeter
(g/cm
3). The preferred polyolefins used in both the base resin and the masterbatch typically
have, before modification with silane functionality, a density of less than 0.930,
preferably less than 0.910, more preferably less than 0.890, even more preferably
less than 0.880 and even more preferably less than 0.870,. The polyolefin copolymers
typically have, before modification with silane functionality, a density greater than
0.850, preferably greater than 0.852 and more preferably greater than 0.855, g/cm
3. Density is measured by the procedure of ASTM D-792. These relatively low density
polyolefins are generally characterized as semi-crystalline, flexible and having good
optical properties, e.g., high transmission of visible and UV-light and low haze.
[0029] The polyolefins used in both the base resin and the masterbatch of this invention
typically have, before modification with silane functionality, a melt index greater
than 0.10 and preferably greater than 1 gram per 10 minutes (g/10 min). The polyolefins
typically have a melt index of less than 75 and preferably of less than 20, g/10 min.
Melt index is measured by the procedure of ASTM D-1238 (190°C/2.16 kg).
[0030] The polyolefins used in both the base resin and the masterbatch of this invention
can be made by any process, e.g., solution, slurry, gas phase, batch, continuous,
high pressure, low pressure, etc., and with any catalyst, e.g., Ziegler-Natta, metallocene,
constrained geometry, etc. In one embodiment, the polyolefins made with Ziegler-Natta
catalysts and under high pressure.
[0031] The polyolefins used in both the base resin and the masterbatch of this invention
include, but are not limited to, ethylene/alpha-olefin interpolymers having an α-olefin
content of between 15, preferably at least 20 and even more preferably at least 25,
weight percent (wt%) based on the weight of the interpolymer. These interpolymers
typically have an α-olefin content of less than 50, preferably less than 45, more
preferably less than 40 and even more preferably less than 35, wt% based on the weight
of the interpolymer. The α-olefin content is measured by
13C nuclear magnetic resonance (NMR) spectroscopy using the procedure described in
Randall (Rev. Macromol. Chem. Phys., C29 (2&3)). Generally, the greater the α-olefin content of the interpolymer, the lower the
density and the more amorphous the interpolymer.
[0032] The α-olefin is preferably a C
3-20 linear, branched or cyclic α-olefin. Examples of C
3-20 α-olefins include propene, 1-butene, 4-methyl-1-pentene, 1-hexene, 1-octene, 1-decene,
1-dodecene, 1-tetradecene, 1-hexadecene, and 1-octadecene. The α-olefins can also
contain a cyclic structure such as cyclohexane or cyclopentane, resulting in an α-olefin
such as 3-cyclohexyl-1-propene (allyl cyclohexane) and vinyl cyclohexane. Although
not α-olefins in the classical sense of the term, for purposes of this invention certain
cyclic olefins, such as norbornene and related olefins, are α-olefins and can be used
in place of some or all of the α-olefins described above. Similarly, styrene and its
related olefins (for example, α-methylstyrene, etc.), and acrylic and methacrylic
acid and their respective ionomers, and acrylates and methacrylates, are α-olefins
for purposes of this invention. Illustrative polyolefin copolymers include ethylene/propylene,
ethylene/butene, ethylene/1-hexene, ethylene/1-octene, ethylene/styrene, and the like.
Ethylene/acrylic acid (EAA), ethylene/methacrylic acid (EMA), ethylene/acrylate or
methacrylate, ethylene/vinyl acetate and the like are also polyolefin copolymers for
purposes of this invention. Illustrative terpolymers include ethylene/propylene/1-octene,
ethylene/propylene/butene, ethylene/butene/1-octene, and ethylene/butene/styrene.
The copolymers can be random or blocky.
[0033] More specific examples of olefinic interpolymers useful in this invention include
very low density polyethylene (VLDPE) (e.g., FLEXOMER® ethylene/1-hexene polyethylene
made by The Dow Chemical Company), homogeneously branched, linear ethylene/α-olefin
copolymers (e.g. TAFMER® by Mitsui Petrochemicals Company Limited and EXACT® by Exxon
Chemical Company), homogeneously branched, substantially linear ethylene/α-olefin
polymers (e.g., AFFINITY® and ENGAGE® polyethylene available from The Dow Chemical
Company), and olefin block copolymers such as those described in USP
7,355,089 (e.g., INFUSE® available from The Dow Chemical Company). The more preferred polyolefin
copolymers are the homogeneously branched linear and substantially linear ethylene
copolymers. The substantially linear ethylene copolymers are especially preferred,
and are more fully described in USP
5,272,236,
5,278,272 and
5,986,028.
[0034] The polyolefin copolymers useful in the practice of this invention also include propylene,
butene and other alkene-based copolymers, e.g., copolymers comprising a majority of
units derived from propylene and a minority of units derived from another α-olefin
(including ethylene). Exemplary propylene polymers useful in the practice of this
invention include the VERSIFY® polymers available from The Dow Chemical Company, and
the VISTAMAXX® polymers available from ExxonMobil Chemical Company.
[0035] Blends of any of the above olefinic interpolymers can also be used in this invention,
and the polyolefin copolymers can be blended or diluted with one or more other polymers
to the extent that the polymers of this invention constitute at least 70, preferably
at least 75 and more preferably at least 80, weight percent of the blend.
Silane Functionality
[0036] The polyolefins used in the base resin of this invention contain, of course, silane
functionality, e.g., alkoxysilane groups. The silane functionality is included in
the polyolefin either through grafting or copolymerization. Any silane that will effectively
graft to the polyolefin or copolymerize with the olefin monomer can be used in the
practice of this invention. Suitable silanes include unsaturated silanes that comprise
an ethylenically unsaturated hydrocarbyl group, such as a vinyl, allyl, isopropenyl,
butenyl, cyclohexenyl or γ-(meth)acryloxy allyl group, and a hydrolyzable group, such
as, for example, a hydrocarbyloxy, hydrocarbonyloxy, or hydrocarbylamino group. Examples
of hydrolyzable groups include methoxy, ethoxy, formyloxy, acetoxy, proprionyloxy,
and alkyl or arylamino groups. Preferred silanes are the unsaturated alkoxy silanes
which can be grafted onto the polymer. These silanes and their method of preparation
are more fully described in USP
5,266,627. Vinyl trimethoxy silane, vinyl triethoxy silane, γ-(meth)acryloxy propyl trimethoxy
silane and mixtures of these silanes are the preferred silane crosslinkers for is
use in this invention.
[0037] Alternatively, silane copolymers, e.g., SILINK™ poly(ethylene-co-vinyltrimethoxysilane)
copolymer, can be used in place of or in combination with polyolefins grafted or otherwise
modified with alkoxysilane groups.
[0038] The amount of units derived from the vinyl silane that are either grafted to or incorporated
into the polyolefin backbone can vary widely depending upon the nature of the polyolefin,
the silane, the processing conditions, the grafting efficiency, the ultimate application,
and similar factors, but typically the amount is at least 0.2, preferably at least
0.5, wt% based on the weight of the polyolefin. Considerations of convenience and
economy are usually the two principal limitations on the maximum amount of units derived
from a vinyl silane grafted to or incorporated into the polyolefin backbone, and typically
the maximum amount of such units does not exceed 5, preferably it does not exceed
3, wt% based on the weight of the polyolefin.
[0039] The vinyl silane is grafted to the polyolefin by any conventional method, typically
in the presence of a free radical initiator e.g. peroxide, or by ionizing radiation,
etc. Organic initiators are preferred, such as any one of the peroxide initiators,
for example, dicumyl peroxide, di-tert-butyl peroxide, t-butyl perbenzoate, benzoyl
peroxide, cumene hydroperoxide, t-butyl peroctoate, methyl ethyl ketone peroxide,
2,5-dimethyl-2,5-di(t-butyl peroxy)hexane, lauryl peroxide, and tert-butyl peracetate.
The amount of initiator can vary, but it is typically present in an amount of at least
0.01, preferably at least 0.03, wt%. Typically, the initiator does not exceed 0.15,
preferably it does not exceed about 0.10, wt%. The weight ratio of vinyl silane to
initiator also can vary widely, but the typical vinyl silane:initiator weight ratio
is between 10:1 to 150:1, preferably between 18:1 and 100:1. The polyolefin can be
grafted with the vinyl silane either (1) before the base resin is formulated, e.g.,
the embodiment in which the base resin comprises a polyolefin containing silane functionality
in combination with a hydroxy-terminated silicone polymer, or (2) after the base resin
is formulated, e.g., the embodiment in which the base resin comprises a blend of a
vinyl silane, polyolefin, organic initiator and a hydroxy-terminated silicone polymer.
In the latter embodiment, the grafting occurs after feeding the tape to the injection
molding machine. In the former embodiment, any conventional method can be used to
graft the silane crosslinker to the polyolefin, and one preferred method is melt blending
in a reactor extruder, such as a twin-screw extruder or a Buss kneader at appropriate
temperatures depending on the polymer and the initiator used.
Hydroxy-Terminated Silicone Polymer
[0040] The selection of suitable hydroxy-terminated silicone polymers for use in this invention
is limited to those silicone polymers that can be blended with either (1) a polyolefin
containing silane functionality, or (2) a mixture of vinyl silane, polyolefin and
peroxide. This ability to mix will typically be affected by the viscosity of the hydroxy-terminated
silicone polymer which generally relates to its molecular weight. Typically, the viscosity
of the hydroxy-terminated silicone polymer ranges from 80 to about 2500 centistokes
(cs). Such viscosities are typical for silicone softeners or lubricants found in the
market.
[0041] Non-limiting examples of useful hydroxy-terminated silicone polymers include those
of the following formula (I):

in which "n" is from 3 to 20, although other hydroxy-terminated silicone polymers
may be employed within the scope of the present invention. Notably, silicone polymers
according to the foregoing formula (I) will have a viscosity in the range of from
80 to 2500 cs.
Catalyst
[0042] The reaction of the polyolefin containing silane functionality with the hydroxy-terminated
silicone polymer is accelerated with a cure catalyst, and any catalyst that will provide
this function can be used in the practice of this invention. These catalysts generally
include organic bases, carboxylic acids and organometallic compounds including organic
titanates and complexes or carboxylates of lead, cobalt, iron, nickel, zinc and tin.
Illustrative catalysts include dibutyl tin dilaurate, dioctyl tin maleate, dibutyl
tin diacetate, dibutyl tin dioctoate, stannous acetate, stannous octoate, lead naphthenate,
zinc caprylate and cobalt naphthenate. Tin carboxylates such as dibutyl tin dilaurate,
dimethyl hydroxy tin oleate, dioctyl tin maleate, di-n-butyl tin maleate and titanium
compounds such as titanium 2-ethylhexoxide are particularly effective for use in this
invention.
Additives
[0043] The polymeric materials, e.g., the base resin and the catalyst masterbatch, of this
invention can comprise additives other than or in addition to cure catalysts. For
example, such other additives include UV-stabilizers and processing stabilizers such
as trivalent phosphorus compounds. The UV-stabilizers include hindered phenols such
as Cyasorb UV2908 and hindered amines such as Cyasorb UV 3529, Hostavin N30, Univil
4050, Univin 5050, Chimassorb UV 119, Chimassorb 944 LD, Tinuvin 622 LD and the like.
The phosphorus compounds include phosphonites (PEPQ) and phosphites (Weston 399, TNPP,
P-168 and Doverphos 9228). The amount of UV-stabilizer is typically from 0.1 to 0.8%,
and preferably from 0.2 to 0.5%. The amount of processing stabilizer is typically
from 0.02 to 0.5%, and preferably from 0.05 to 0.15%.
[0044] Still other additives include, but are not limited to, antioxidants (e.g., hindered
phenolics such as Irganox® 1010 made by Ciba Geigy Corp.), cling additives (e.g.,
polyisobutylene), anti-blocks, anti-slips, pigments, fillers (clear if transparency
is important to the application), surfactants, and flame retardants. In-process additives,
e.g. calcium stearate, water, etc., may also be used. These and other potential additives
are used in the manner and amount as is commonly known in the art.
[0045] Carbon black is a common filler and/or pigment for the polymeric materials used in
the practice of this invention. Any carbon black can be used and for those applications
in which the finished polymeric material requires some measure of conductivity, e.g.,
cable coverings, the carbon black preferably exhibits at least a low level of electrical
conductivity. For example, if the polymeric material is to be used as a semiconductor
shield for a cable, then preferably the carbon black will reduce the electrical conductivity
of the polymeric material to less than 500 ohm-meter, more preferably to less than
250 ohm-meter, and even more preferably to less than 100 ohm-meter.
[0046] Examples of carbon blacks that can be used in the practice of this invention include
furnace black, acetylene black, kettchen black, channel black and thermal black. Commercially
available carbon blacks include N550 carbon black sold by Cabot Corporation. The amount
of carbon black admixed with the base resin, if any, is typically from 20 to 90 parts
by weight and preferably from 40 to 80 parts by weight.
Compounding the Base Resin and the Catalyst Masterbatch.
[0047] Both the base resin and the catalyst masterbatch are compounded using standard equipment
and techniques. Examples of compounding equipment are internal batch mixers, such
as a Banbury™ or Boiling™ internal mixer. Alternatively, continuous single, or twin
screw, mixers can be used, such as Farrel™ continuous mixer, a Werner and Pfleiderer™
twin screw mixer, or a Buss™ kneading continuous extruder. The type of mixer.utilized,
and the operating conditions of the mixer, will affect properties of the material
under mixture, such as viscosity, volume resistivity, and extruded surface smoothness.
[0048] In a preferred embodiment, the formulation of the base resin, either (1) a polyolefin
containing silane functionality and a hydroxy-terminated silicone polymer, or (2)
a polyolefin, vinyl silane, an optional organic initiator, and hydroxy-terminated
silicone polymer, are added to a mixing vessel in any order and in the appropriate
amounts, and mixed under non-reactive conditions to form an essentially homogeneous
mixture of the components. The amount by weight of polyolefin (with or without silane
functionality) to hydroxy-terminated silicone polymer in the mixture is typically
in the range of 50:50, more typically 80:20 and even more typically 95:5.
[0049] In the formulation of the catalyst masterbatch, a large amount of cure catalyst is
mixed with a representative portion of the carrier polymer, typically the same polyolefin
used in the base resin but without silane functionality, to form a substantially homogeneous
mixture. The amount of catalyst to carrier resin in the mixture can vary widely, but
is typically 10:90, more typically 5:95 and even more typically 3:97.
Manufacture of the Tape
[0050] After the base resin is formed into an essentially homogeneous mixture, including
any additives, it is extruded into a tape, i.e., a continuous strip, and allowed to
solidify. The dimensions of the tape can vary widely, but typical tapes have a width
dimension of between 50 and 10 millimeters (mm), a thickness dimension of between
2 and 20 mm, and an indefinite length, i.e., a length of choice that is limited only
by the volume of mixture extruded. The tape can have any one of a number of different
configurations. Figure 1A illustrates base resin tape 10 in an essentially smooth
and flat configuration and comprising a single layer. Alternatively and not shown,
tape 10 can comprise a stack of multiple micro-layers which, in the aggregate, have
a thickness comparable to that of single layer tape 10. Such tapes are well-known
in the art, and are illustrated in USP
5,094,793.
[0051] Figure 1B shows the tape 10 configured with continuous machine-direction groove 11a.
Figure 1C shows tape 10 configured with intermittent or discontinuous machine-direction
groove 11b. Figure 1D shows tape 10 configured with cross-direction grooves 11c. The
groove or grooves can also be at other angles to the machine direction of the ribbon.
The depth, cross-section configuration (e.g., V-shaped, U-shaped, etc.), shape (e.g.,
straight, serpentine, etc.,), etc., of the groove can vary to choice with the understanding
that the groove is preferably configured to received and physically (as opposed to
chemically or adhesively) hold the catalyst masterbatch component of the finished
tape product. For reasons of ease of manufacture, equipment selection and the like,
preferably tape 10 is configured with a continuous, machine-direction groove.
[0052] Typically, the catalyst masterbatch is also extruded as a continuous strip, typically
a strip much smaller in width and physically adjoined to the tape in any suitable
manner. Here too, the strip can comprise a single layer or a stack of micro-layers.
If the tape is not configured with a groove or similar device to receive and hold
the catalyst masterbatch, then typically it is simply laid upon the solidified base
resin tape and through the combination of (i) any inherent tackiness between the base
resin tape and catalyst masterbatch ribbon, and (ii) the physical restraint resulting
from the collection of the tape and ribbon into a reel. Alternatively, or in addition
to, the catalyst masterbatch ribbon can be pressed, with or without heating, against
the base resin tape, e.g., by passing the combination of the two through one or more
sets of pinch rollers, to promote the joining of the two components. If heat is used,
then only sufficient heat to soften one or both of the base resin tape or catalyst
masterbatch ribbon is used. Full melting of either the base resin tape or the catalyst
masterbatch ribbon is not desirable.
[0053] Similarly, an adhesive can be employed to fix the catalyst masterbatch to the base
resin tape. If an adhesive is used, then only an amount sufficient to promote the
adhesion of the catalyst masterbatch ribbon to the base resin tape is employed. The
adhesive can be employed congruent with the catalyst masterbatch ribbon, or intermittent
with it. The choice of adhesive, if any, is not critical to the practice of this invention
and as such, any adhesive that does not materially adversely impact the desired polymeric
properties can be used. Typically, the adhesive is a pressure-sensitive adhesive;
preferably a natural or synthetic rubber used either alone or in combination with
one or more other adhesives. The acrylate and methacrylate-based adhesives are also
useful in the practice of this invention. The adhesive can be applied as a coating,
separate ribbon (e.g., lamination), or by any other convenient method. It can be applied
to the full surface area of the base resin tape, or limited to the groove or grooves,
or applied to the catalyst masterbatch ribbon, or both.
[0054] If the base resin tape is configured with a groove or similar device, particularly
a continuous, machine-direction groove, then the catalyst masterbatch is sized for
and extruded in a manner that allows insertion into the groove. Here too, insertion
of the catalyst masterbatch ribbon into the groove on the base resin tape can be aided
through the application of pressure, e.g., the use of one or more sets of pinch rollers.
Figure 2A illustrates continuous catalyst masterbatch ribbon 12 inserted into continuous
machine-direction groove 11a (not shown) of tape 10. Although the catalyst masterbatch
strip can also be of indefinite length, it can also be much shorter and fitted to
the base resin tape on an intermittent or discontinuous basis as illustrated in Figure
2B. The catalyst masterbatch is fitted to the base resin tape such that it represents
3 to 5 wt% of the combined weight of the base resin and catalyst masterbatch so as
not to interfere with crosslinking efficiency of the base resin tape.
[0055] In an alternative embodiment base resin tape 10 and catalyst masterbatch ribbon 12
are separated by intermediate barrier layer 13 as illustrated in Figure 3. Here too,
the barrier resin layer can be a single layer or a stack of micro-layers. This intermediate
layer can comprise any material that will delay the contact of the catalyst of the
masterbatch with the base resin tape. Such materials include, but are not limited
to, functional copolymers, e.g., nylon, Saran, ethylene vinyl alcohol copolymer, and
the like. In this embodiment, the final product tape, i.e., the tape comprising the
three layers of base resin, barrier resin and catalyst masterbatch, is typically a
multilayered structure with each layer of approximately the same width and length
although the thickness of each layer is likely different with the base resin layer
the thickest and the catalyst masterbatch layer the thinnest. The presence of the
intermediate barrier layer enhances the life of the final product tape by preventing
premature reaction (scorching) of the polyolefin containing silane functionality and
the hydroxy-terminated silicone polymer until the tape is fed to an extruder and the
tape components melt blended with one another prior to extrusion.
[0056] In another embodiment the catalyst masterbatch, or simply and preferably just catalyst,
is dosed onto the base resin ribbon just prior to or simultaneously with the feeding
of the ribbon to an extruder. This embodiment is illustrated by the schematic of Figure
4. Base resin ribbon 10 is fed directly to extruder 16. As the base resin ribbon is
fed into the injection molding machine, the tape is dosed, e.g., sprayed, with catalyst
14 from pump or other delivery device 15. Since shelf life of the final product tape,
e.g., base resin ribbon and catalyst, is not a concern in this embodiment, neither
a carrier resin nor a barrier layer is required. However, this embodiment does encourage
preparation of the final tape product at the site of the extrusion or molding operation
(although the tape will have a limited shelf life under the ambient conditions that
prevail outside of the extruder).
[0057] Alternative dosing methods include passing the base resin tape through a bath comprising
the catalyst prior to feeding the tape to an injection molding machine, depositing
catalyst in the form of a full or partial coating onto the base resin tape by any
coating technique, and feeding the catalyst, either neat or in the form of a masterbatch,
directly into the injection molding machine apart from but simultaneously with or
prior to the feeding of the base resin tape to the injection molding machine. Conventional
injection molding machines typically have a zone or compartment in which components
of a formulation can be homogeneously blended before transferred to the mold or extruder,
and to this zone or compartment is where the base resin tape and catalyst are fed.
[0058] Current rubber injection molding technology uses tapes made from pre-compounded and
fully homogenized peroxide based materials. While these materials have a relatively
good shelf life when stored at room temperature, this approach is not useful with
materials that inherently reactive materials over a broad range of temperatures. The
tapes and processes of this invention are particularly useful in the field of moisture-curable
or hydroxy-silicone cured resins systems and applications.
[0059] Although the invention has been described in considerable detail through the preceding
description, drawings and examples, this detail is for the purpose of illustration.
One skilled in the art can make many variations and modifications without departing
from the spirit and scope of the invention as described in the appended claims.